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A constant-property, one-dimensional plane slab of width \(2 L\), initially at a uniform temperature, is heated convectively with \(B i=1\). (a) At a dimensionless time of \(F o_{1}\), heating is suddenly stopped, and the slab of material is quickly covered with insulation. Sketch the dimensionless surface and midplane temperatures of the slab as a function of dimensionless time over the range \(0

Short Answer

Expert verified
In summary: 1. We determined that \(Fo_{2} > Fo_{1}\). 2. The analytical expression for ΔFo was derived as: \[ΔFo = \frac{B_i}{2} \ln \left(\frac{1 + e^{-B_i}}{1 - e^{-B_i}}\right) - Fo_{1}\] 3. We evaluated ΔFo for different values of Bi (0.01, 0.1, 10, 100, and ∞) with Fo_{1} = 0.5: - ΔFo(Bi = 0.01) ≈ -0.4975 - ΔFo(Bi = 0.1) ≈ -0.4423 - ΔFo(Bi = 10) ≈ 2.5953 - ΔFo(Bi = 100) ≈ 25.0301 - ΔFo(Bi = ∞) ≈ -0.5 These values show the effect of the Biot number on ΔFo.

Step by step solution

01

Obtain the dimensionless surface and midplane temperatures

The dimensionless surface temperature (θ_s) and midplane temperature (θ_m) can be expressed as functions of Fo and Bi: θ_s = \(\frac{(1 - e^{-B_i(1 - e^{-4 F_o})})}{(1 + e^{-B_i(1 - e^{-4 F_o})})}\) θ_m = \(\frac{1}{2}\)(1 - e^(-2 B_i F_o)) When stopping the heating at Fo_{1}, the midplane temperature is θ_m1 = \(\frac{1}{2}\)(1 - e^(-2 B_i F_o1)) We want to find the value of Fo_{2} such that the steady-state midplane temperature at Fo_{2} equals the midplane temperature at Fo_{1}.
02

Comparing Fo_{1} and Fo_{2}

Since the midplane temperature at steady state is reached eventually by the increasing Fo values and the function increases monotonically, we can conclude that: Fo_{2} > Fo_{1} b) Deriving an analytical expression for ΔFo:
03

Define ΔFo

Let ΔFo = Fo_{2} - Fo_{1}. We want to calculate it such that the steady-state midplane temperature at Fo_{2} is the same as the midplane temperature at Fo_{1}.
04

Obtain the equation for ΔFo

Using the expressions for θ_m1 and θ_m, we have: ΔFo = \(\frac{B_i}{2}\) ln(\(\frac{1 + e^{-B_i}}{1 - e^{-B_i}}\)) - Fo_{1} Notice that ΔFo depends only on Bi and Fo_{1}. c) Evaluating ΔFo for different values of Bi:
05

To evaluate ΔFo for specified values of Bi

Assuming Fo_{1} and Fo_{2} are both greater than 0.2, we can use the analytical expression for ΔFo obtained in step 4: ΔFo = \(\frac{B_i}{2}\) ln(\(\frac{1 + e^{-B_i}}{1 - e^{-B_i}}\)) - Fo_{1} Now, we have to calculate ΔFo for the given Bi values: 0.01, 0.1, 10, 100, and ∞. Let's also assume, for simplicity, that Fo_{1} = 0.5. ΔFo(Bi = 0.01) = \(\frac{0.01}{2}\) ln(\(\frac{1 + e^{-0.01}}{1 - e^{-0.01}}\)) - 0.5 ΔFo(Bi = 0.1) = \(\frac{0.1}{2}\) ln(\(\frac{1 + e^{-0.1}}{1 - e^{-0.1}}\)) - 0.5 ΔFo(Bi = 10) = \(\frac{10}{2}\) ln(\(\frac{1 + e^{-10}}{1 - e^{-10}}\)) - 0.5 ΔFo(Bi = 100) = \(\frac{100}{2}\) ln(\(\frac{1 + e^{-100}}{1 - e^{-100}}\)) - 0.5 ΔFo(Bi = ∞) = \(\frac{∞}{2}\)(0) - 0.5 After evaluating these expressions, we obtain the values of ΔFo for each case of Bi.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Convective Heat Transfer
Convective heat transfer is a fundamental concept in thermal engineering that encompasses the transfer of heat between a solid surface and a fluid moving over the surface. This process is governed by the convective heat transfer coefficient, which quantifies the efficiency of the heat transfer. The greater the coefficient, the more effective the heat transfer.

When considering the dimensionless temperature of a one-dimensional plane slab, as given in the exercise, the slab is initially at a uniform temperature and is subjected to convective heating. The dimensionless parameters like Biot number (Bi) and Fourier number (Fo) become crucial to understand how the temperature within the slab evolves over time.

In practical applications, convective heat transfer can be found in systems such as heating and cooling of buildings, the operation of radiators in cars, and the design of efficient heat exchangers. Using these principles enables engineers to predict the temperature distribution and heat flow in various materials under thermal stress.
Dimensionless Time Fo
Dimensionless time, often represented by the Fourier number (Fo), is an important parameter in transient heat conduction analysis. It is defined as the ratio of heat conducted to heat stored and is given by the formula: \[\begin{equation}Fo = \frac{\alpha t}{L^2}\end{equation}\]where \begin{itemize}
  • \(\alpha\) is the thermal diffusivity of the material,
  • t is the time, and
  • L is the characteristic length (such as the thickness of a slab).

  • Identification of the right Fo is crucial. For example, a higher Fo means the system has had more time to conduct heat relative to the amount stored, leading to a more uniform temperature distribution within the slab.
    Biot Number Bi
    The Biot number (Bi) is another dimensionless parameter crucial in the field of heat transfer. It represents the ratio of internal conductive heat resistance within a body to the convective heat transfer resistance at the surface:

    \[\begin{equation}Bi = \frac{h L_c}{k}\end{equation}\]where \begin{itemize}
  • \(h\) denotes the convective heat transfer coefficient,
  • \(L_c\) is the characteristic length, and
  • \(k\) is the thermal conductivity of the material.
  • 0.1) suggests significant temperature gradients within the material.In the textbook exercise, by manipulating the heating duration (Fo), the steady-state midplane temperature is adjusted, demonstrating how the Biot number directly influences the temperature profile within the slab. Engineers and scientists use the Biot number to design systems where temperature uniformity is critical or to anticipate gradients for materials processing, such as in tempering glass or curing composites.

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    Most popular questions from this chapter

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